EP0304207A2 - Cartouche filtrante à grande superficie - Google Patents

Cartouche filtrante à grande superficie Download PDF

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Publication number
EP0304207A2
EP0304207A2 EP88307314A EP88307314A EP0304207A2 EP 0304207 A2 EP0304207 A2 EP 0304207A2 EP 88307314 A EP88307314 A EP 88307314A EP 88307314 A EP88307314 A EP 88307314A EP 0304207 A2 EP0304207 A2 EP 0304207A2
Authority
EP
European Patent Office
Prior art keywords
filter
layers
filter cartridge
filter media
cartridge according
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
EP88307314A
Other languages
German (de)
English (en)
Other versions
EP0304207B1 (fr
EP0304207A3 (en
Inventor
Yuan-Ming C/O Minnesota Mining And Tang
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
3M Co
Original Assignee
Minnesota Mining and Manufacturing Co
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Minnesota Mining and Manufacturing Co filed Critical Minnesota Mining and Manufacturing Co
Publication of EP0304207A2 publication Critical patent/EP0304207A2/fr
Publication of EP0304207A3 publication Critical patent/EP0304207A3/en
Application granted granted Critical
Publication of EP0304207B1 publication Critical patent/EP0304207B1/fr
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D29/00—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor
    • B01D29/44—Edge filtering elements, i.e. using contiguous impervious surfaces
    • B01D29/46—Edge filtering elements, i.e. using contiguous impervious surfaces of flat, stacked bodies
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D29/00—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor
    • B01D29/11—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor with bag, cage, hose, tube, sleeve or like filtering elements
    • B01D29/31—Self-supporting filtering elements
    • B01D29/35—Self-supporting filtering elements arranged for outward flow filtration
    • B01D29/353—Self-supporting filtering elements arranged for outward flow filtration with corrugated, folded filtering elements
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D29/00—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor
    • B01D29/01—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor with flat filtering elements
    • B01D29/05—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor with flat filtering elements supported
    • B01D29/07—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor with flat filtering elements supported with corrugated, folded or wound filtering sheets
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D29/00—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor
    • B01D29/11—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor with bag, cage, hose, tube, sleeve or like filtering elements
    • B01D29/13—Supported filter elements
    • B01D29/15—Supported filter elements arranged for inward flow filtration
    • B01D29/21—Supported filter elements arranged for inward flow filtration with corrugated, folded or wound sheets
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D29/00—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor
    • B01D29/11—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor with bag, cage, hose, tube, sleeve or like filtering elements
    • B01D29/13—Supported filter elements
    • B01D29/23—Supported filter elements arranged for outward flow filtration
    • B01D29/232—Supported filter elements arranged for outward flow filtration with corrugated, folded or wound sheets
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D29/00—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor
    • B01D29/11—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor with bag, cage, hose, tube, sleeve or like filtering elements
    • B01D29/31—Self-supporting filtering elements
    • B01D29/33—Self-supporting filtering elements arranged for inward flow filtration
    • B01D29/333—Self-supporting filtering elements arranged for inward flow filtration with corrugated, folded filtering elements
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2201/00—Details relating to filtering apparatus
    • B01D2201/18—Filters characterised by the openings or pores
    • B01D2201/182—Filters characterised by the openings or pores for depth filtration

Definitions

  • the present invention relates to filter cartridges for fluids and more particularly to high surface area, replaceable filter cartridges for gas or liquid filtration applications.
  • a generally cylindrical filter cartridge is produced from a flat paper filter sheet in which the connecting area between pleats has a series of tucks which allow the course of the pleats to be reversed without cutting the filter paper.
  • a more conventional approach to increasing the available filtration area while minimizing the volume of the filter unit involves the use of longitudinal, accordion pleats wherein the filter media is folded into a pleated structure and formed into a generally cylindrical shape.
  • U.S. Patent 3,867,294 and EP 44,042 disclose two of many variations of this basic concept.
  • the present invention relates to high surface area per unit volume, generally cylindrical filter cartridges for gaseous or liquid fluid filtration.
  • These filter cartridges comprise a nested arrangement of disk shaped filter layers having a radial pleat pattern comprising a pattern of regular radial pleats.
  • a secondary pattern of irregular wave like radial pleats generally results from packing of the structure around the inner circumference of the disk shaped layers to form the filter cartridge.
  • a principal objective of the present invention is to provide a filter cartridge having a higher surface area per unit volume than is possible with conventional pleated cartridges.
  • the surface area of the filter cartridges of the present invention can be controlled over a wide range simply by varying the packing or nesting density of the disk shaped layers. Additionally, the nesting density can be controlled in a continuous or discontinuous manner over the length of the filter cartridge so as to produce filter cartridges having a uniform or gradient distribution of filter media over the length of the cartridge.
  • filter cartridges are prepared from tubular elements generated from flat filter media having embossed thereon a series of transverse raised and recessed shapes.
  • the disk shaped layers of the filter cartridges of the present invention are generated by folding the tubular elements to produce composite radially pleated disk shaped layers.
  • the filter cartridge has a generally cylindrical shape and comprises a filter element having a multiplicity of layers of filter media of increasingly finer downstream porosity.
  • the filter media is preferably a nonwoven material, and more preferably, a nonwoven microfiber web or a fibrillated film web.
  • a series of nonwoven webs, including an upstream prefilter layer, fine particle filtration media and a downstream cover layer, are seamed together by one or more fluid impervious seams to produce a flat tubular element which is then embossed through the application of heat and pressure.
  • the resulting embossed structure is opened, folded and longitudinally collapsed to form a generally cylindrical filter element comprised of stacked disk shaped layers.
  • Filter cartridges are prepared from the longitudinally collapsed filter elements by inserting the filter elements into a preformed cartridge or by attaching endpieces to the filter elements by means of fluid impervious seals.
  • Alternative cartridge filter constructions wherein one end of the filter element is sealed to itself rather than to an endpiece, are also possible with the present invention.
  • inner and outer support structures may be added to the filter cartridge assembly to provide supplemental support to the cartridge to assist in maintaining its shape in high pressure filtration applications.
  • the filter cartridges of the present invention can be readily adapted to either an inward-out or an outward-in flow configuration.
  • the filter cartridges of the present invention comprise a filter element of nested substantially disk shaped layers having a radial pleated pattern, said filter cartridges having higher surface areas per unit volume than conventionally pleated filter cartridges.
  • the filter cartridges are readily adapted to filtration applications involving either gaseous or liquid fluids.
  • a variety of filter media, including paper, woven or nonwoven webs, sorbent loaded webs, permeable membranes and porous metals can be utilized in the present invention.
  • FIG. 1 illustrates a cross-section of one embodiment of the invention in which the filter element 10 comprises a coarse upstream prefilter layer 11, filtration media 12 comprising a multiplicity of filter media layers having increasingly finer downstream porosity, and a downstream cover layer 13.
  • Suitable materials for the upstream prefilter layer include thermoplastic scrims, thermoplastic spunbond webs or staple fiber nonwoven webs having thermoplastic binder systems.
  • nonwoven materials or permeable membranes are the materials of choice.
  • the nonwoven materials are typically fibrous webs having an average fiber diameter of less than about 100 microns or fibrillated film webs such as those described in U.S. Re. 31,285.
  • Fibrous filtration media based on polyolefins e.g., polyethylene, polypropylene
  • polyesters e.g., polyethylene terephthalate
  • polycarbonate e.g., polycarbonate
  • the fine particle filtration media are typically in the form of microfiber webs or blown microfiber webs having an average fiber diameter of less than about 10 microns.
  • Blown microfiber webs can be conveniently prepared according to the procedures taught by Wente, Van A., "Superfine Thermoplastic Fibers” in Industrial Engineering Chemistry , Vol. 48, 1342 et seq (1956), and when they are prepared in persistent electrically charged form (see Kubik et al, U.S. Patent 4,215,682), they are especially useful.
  • Permeable membranes such as a Metricel polypropylene membrane (0.2 pore size, available from Gelman, Ann Arbor, Michigan, U.S.A.) or the membrane material described in U.S. Patent 4,613,544 are particularly well suited as filter media for the present invention.
  • Suitable materials for the downstream cover layer 13 include finish free, low debris thermoplastic webs such as spunbond webs or nonwoven webs based on thermally activated binder fibers such as spunbond polypropylene webs.
  • Tubular filter elements 30 formed from filter media laminates illustrated in FIG. 1 are prepared by folding a laminate over upon itself or stacking two laminates with their downstream cover layers 13 adjacent to each other and joining the free edge(s) together by means of a fluid impervious longitudinal seal 25 as illustrated in FIG. 2.
  • a number of techniques are applicable to the formation of this seal including, but not limited to, adhesive bonds, heat sealing, mechanical bonding, thermo-mechanical bonding or ultrasonic welding. More complex, multi-lobal filter shapes having a generally cylindrical overall shape requiring more than two sections of filter media laminates and a multiplicity of longitudinal fluid impervious bonds are also possible with the filters of the present invention.
  • Preparation of filter elements 30 from substantially flat filter media requires that the media have a regular pattern of transverse and longitudinal forming lines on the filter media which define fold lines for creating the disk shaped layers and the primary radial pleat pattern which is superimposed on those elements.
  • the forming line pattern can consist simply of a series of lines embossed on the filter media or by introducing a multiplicity of transverse rows of raised and recessed shapes on the filter media. Either alternative can be developed as a part of the manufacturing process for the media or introduced into the media prior to assembling the filter laminate.
  • the filter laminate may be assembled and the desired line or shape pattern imparted to it by an embossing operation.
  • a variety of geometric shapes including regular shapes (e.g., partial cylinders, squares, rectangles and triangles) or irregular shapes can be embossed on the filter laminates.
  • the shapes must be arrayed such that, on the unopened tubular element, it defines a series of transverse lines, which correspond to the fold lines that create the disk shaped layers, and a series of longitudinal lines, which define fold lines that create the primary regular radial pleat pattern on the disk shaped layers.
  • Embossed media is preferred to lined media for forming the filter elements of the present invention as the embossed media produces a more uniform primary radial pleat pattern due to the fact that the raised and recessed shapes provide a predetermined alternating folding direction for the media during the folding operation. Additionally, the regularity of the primary radial pleat pattern facilitates packing or nesting of adjacent disk shaped layers which enables higher surface area per unit volume to be achieved.
  • FIG. 2 One embodiment of an embossed pattern on the filter laminate which produces the unique folding pattern for filters of the present invention is illustrated in FIG. 2.
  • the filter laminate 20 has a multiplicity of rows of alternating raised 21 and recessed 22 partially cylinders. Adjacent transverse rows of the embossed units are offset from each other by a distance corresponding to the width of the partial cylinder. This displacement results in a series of transverse, wave shaped lines 23 described by the junction of adjacent rows of partial cylinders which, in turn, defines the inward and outward fold lines that create the disk shaped layers of the longitudinally collapsed tubular filter element.
  • the height of the partial cylinder which is typically less than about 50% of the radius of the collapsed cylindrically shaped tubular filter element, determines the depth of the transverse pleats. Regions where the raised partial cylinders transition into the recessed partial cylinders describe a series of longitudinal lines 24 which define the fold lines of the primary regular radial pleat pattern that is superimposed on the disk shaped layers of the filter.
  • Filter elements 30 of the present invention are prepared from embossed tubular laminate elements 20 illustrated in FIG. 2 by opening the tubular element and initiating an alternating inward/outward folding of adjacent transverse lines of the laminate which causes a longitudinal collapse of the tubular element and concurrent formation of the disk shaped layers 31 of the filter structure. Interaction of the longitudinal lines 24 of the laminate with the transverse lines during the folding operation produces the primary regular radial pleat pattern 32. Packing of the filter media around the inner circumference of the filter causes the primary radial pleat pattern 32 to form a secondary, irregular wave-like radial pleat pattern 33. The irregular pattern of the secondary radial pleat pattern 33 can manifest itself over the total disk shaped layer, but it typically has its maximum amplitude around the inner circumference of the filter.
  • the primary and secondary radial pleat patterns 32, 33 of adjacent disk layers creates a series of channels 34 leading into the central portion of the filter element which evenly distributes the fluid over the total filter element. This feature enables the filters of the present invention to utilize essentially all of the area of the filter media which correspondingly leads to higher loading capacities per unit volume than can be achieved with conventional pleated filter cartridges.
  • a range of diameters of filter cartridges can be prepared from the same tubular element by initiating the inward/outward folding action on non-adjacent transverse fold lines on the tubular element.
  • filter cartridges having a pleat depth 2X or 3X that obtained from folding on adjacent transverse lines can be obtained.
  • Alternative structures can also be created from the same tubular element by involving a mixed pattern of adjacent and non-adjacent transverse fold lines in the inward/outward folding pattern.
  • Filter elements of the present invention are typically assembled into cartridge units in which the filter element is attached to endpieces by means of fluid impervious bonds.
  • a number of techniques are suitable for this attachment, including adhesive attachment, solvent welding, mechanical attachment, thermo-mechanical attachment or ultrasonic welding.
  • the endpieces of the cartridge are fitted with a means for introducing or removing fluids to or from the interior of the filter cartridge.
  • An alternative construction of the filter cartridge involving the use of a single endpiece and sealing the opposite end of the filter element to itself by means of a fluid impervious bond similar to that used in the longitudinal seam formation is also possible.
  • the filter elements of the present invention can be made substantially self-supporting by the appropriate selection of prefilter materials, filtration media and downstream cover materials. However, in many applications it is desirable to provide additional internal or external support for the filter element. Under these circumstances a supplemental support structure 40 similar to that illustrated in FIG. 4 may be advantageously incorporated into the filter cartridge assembly.
  • An external support 41 such as a screen or casing with a multiplicity of holes can provide additional support in an inward-out fluid flow mode to reduce the likelihood of the filter element rupturing.
  • an inner support structure 42 consisting of a screen, a porous casing or similar constructions can provide support to prevent the filter element from collapsing under high pressure applications in an outward-in fluid flow situation. In both cases, the supplemental support structure is normally attached to the endpiece 43 of the cartridge assembly to provide an integral unit.
  • Two layers of a laminated filter media consisting of a prefilter of polypropylene scrim (Conwed XN-3232, available from Conwed Corp.), two layers of polypropylene blown microfiber web (40 gm/m2 basis wt., each approximately 0.018 cm thick), and a downstream cover layer of spunbond polypropylene (Lutrasil 5020, available from Lutravil Co.), were brought together with the spunbond cover layers in contact with one another and the composite passed through a Branson Sonic Welder in a continuous welding mode (approximately 20-25 psi pressure) to form a series of parallel bond lines spaced approximately 11.43 cm apart, thereby forming a continuous unopened tube.
  • a prefilter of polypropylene scrim Conwed XN-3232, available from Conwed Corp.
  • two layers of polypropylene blown microfiber web 40 gm/m2 basis wt., each approximately 0.018 cm thick
  • a single tubular element was separated from the tube and embossed with a pattern of alternating raised and recessed partial cylindrical shapes approximately 0.4 cm high and 0.5 cm wide (the partial cylinder was approximately 1.65 cm long and had a radius of approximately 0.25 cm) by passing the tubular element through a roller assembly having a heated (approximately 85°C) patterned melt roller.
  • the roller assembly was adjusted to maintain approximately 0.7 kg/cm2 pressure on the tubular element during the embossing process.
  • the embossed element was opened between the two spunbond cover layers and placed over an approximately 3.5 cm diameter support tube to form a generally cylindrical tubular element. Two intersecting wire loops were positioned over a transverse line 24 just beneath the support tube.
  • An approximately 24 cm x 400 cm laminate construction consisting of an upstream prefilter of polypropylene scrim (Conwed XN-3232), a filtration layer of polypropylene blown microfibers (40 gm/m2 basis wt., each approximately 0.018 cm thick) and a downstream cover layer of spunbond polypropylene (Lutrasil 5020, available from Lutravil Co.), was folded over on itself to form an approximately 12 cm x 400 cm sandwich having the downstream cover layer as the central layers.
  • the free edge of the folded sandwich was ultrasonically welded together using a Branson Sonic Welder (continuous welding mode, approximately 20-25 psi pressure) to form an unopened tubular element.
  • the tubular element was embossed, folded and compressed as described in Example 1 to form a cylindrically shaped filter element approximately 7 cm in diameter and 25 cm long. Endpieces were attached to the filter element by potting the filter element in hot melt adhesive in each endpiece.
  • a filter element similar to that described in Example 1 but having a surface area of 0.623 m2 was prepared using 40 gm/m2 basis weight (0.018 cm thick) polypropylene web as the filtration layer.
  • the filter cartridge was compared to a conventional pleated filter cartridge having the same filter media and external dimensions but a surface area of 0.464 m2, for their ability to filter AC Fine Air Cleaner Test Dust (available from A.C. Spark Plug Division, General Motors Corp.), from a stream of water at a flow rate of 11.4 liters per minute. Results of the comparison are shown in Table 1.
  • a filter element similar to that described in Example 1 but having a surface area of 0.625 m2 was prepared and compared to the best performing commercially available conventional 5 ⁇ m pleated filter construction of the same external dimensions in their ability to filter AC Fine Air Cleaner Test Dust from a stream of water at a flow rate of 11.4 liters per minute. Results of this comparison are shown in Table 2.
  • a filter element similar to that described in Example 1 but having a surface area of 0.83 m2 was prepared and compared to the best performing commercially available conventional 10 ⁇ m pleated filter constructions of the same external dimensions in their ability to filter AC Fine Air Cleaner Test Dust from a stream of water at a flow rate of 11.4 liters per minute. Results of this comparison are shown in Table 3. TABLE 3 Filter New Design Commercial Filter P Commercial Filter G Commercial Filter M Surface area (m2) 0.83 0.51 0.46 0.51 Loading (gm) 336 110 50 102 % Efficiency 95 98 95 98
  • the filter cartridge of the present invention has been illustrated and described herein as being tubular and/or generally cylindrical, the cartridge may readily be formed with other cross-sectional shapes such as squares, rectangles, multi-lobed or generally triangular, etc., and such other shapes are contemplated to be encompassed within the terms tubular and/or generally cylindrical.

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Filtering Of Dispersed Particles In Gases (AREA)
  • Filtering Materials (AREA)
  • Filtration Of Liquid (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)
EP88307314A 1987-08-20 1988-08-08 Cartouche filtrante à grande superficie Expired - Lifetime EP0304207B1 (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US87204 1987-08-20
US07/087,204 US4842739A (en) 1987-08-20 1987-08-20 High surface area filter cartridge

Publications (3)

Publication Number Publication Date
EP0304207A2 true EP0304207A2 (fr) 1989-02-22
EP0304207A3 EP0304207A3 (en) 1989-06-14
EP0304207B1 EP0304207B1 (fr) 1993-02-10

Family

ID=22203715

Family Applications (1)

Application Number Title Priority Date Filing Date
EP88307314A Expired - Lifetime EP0304207B1 (fr) 1987-08-20 1988-08-08 Cartouche filtrante à grande superficie

Country Status (9)

Country Link
US (1) US4842739A (fr)
EP (1) EP0304207B1 (fr)
JP (1) JP2698984B2 (fr)
KR (1) KR970002181B1 (fr)
AU (1) AU607519B2 (fr)
BR (1) BR8804189A (fr)
CA (1) CA1317895C (fr)
DE (1) DE3878347T2 (fr)
ES (1) ES2037837T3 (fr)

Cited By (3)

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EP0730490A4 (fr) * 1993-03-24 1997-04-02 Pall Corp Structure composite et son procede d'elaboration
CN102949903A (zh) * 2011-08-18 2013-03-06 通用电气公司 用于与褶式过滤筒一起使用的过滤芯
CN107823961A (zh) * 2013-04-23 2018-03-23 曼·胡默尔有限公司 过滤介质、特别是空气过滤介质以及具有过滤介质的过滤元件、特别是空气过滤元件

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US5543047A (en) 1992-11-06 1996-08-06 Pall Corporation Filter with over-laid pleats in intimate contact
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Publication number Publication date
DE3878347D1 (de) 1993-03-25
EP0304207B1 (fr) 1993-02-10
EP0304207A3 (en) 1989-06-14
AU607519B2 (en) 1991-03-07
JPS6470115A (en) 1989-03-15
AU1974188A (en) 1989-02-23
KR890003428A (ko) 1989-04-14
US4842739A (en) 1989-06-27
CA1317895C (fr) 1993-05-18
KR970002181B1 (ko) 1997-02-25
DE3878347T2 (de) 1993-07-22
JP2698984B2 (ja) 1998-01-19
ES2037837T3 (es) 1993-07-01
BR8804189A (pt) 1989-03-14

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